Improved methods for investigating the external redox potential in hybridoma cell culture

Because of the interest in understanding and optimizing secretion of proteins from mammalian cells, reliable and more reproducible methods are needed to monitor the external redox potential of animal cells in suspension culture. An improved off-line method was established that greatly reduces the typically long response time of redox electrodes in cell culture media and improves the standardization of redox probes. In addition, the dependence of medium redox potential on dissolved oxygen concentrations and pH was investigated using cell-free medium. Off-line as well as on-line redox potential measurements were then applied to spinner or bioreactor cultures of murine hybridoma cells. Serum containing or protein-free medium were used. The time dependence of the experimentally determined external redox potential was found to be affected not only by oxygen, pH, and medium composition. but to a significant extent by the rate of generation of reductants by hybridoma cells. The observed specific rate of medium reduction by generation of reductants (mV h^–1 viable cell^–1) decreased during exponential growth while cell number increased from 2×10⁵ viable cells ml^–1 to 3.5×10⁶ viable cells ml^–1. This rate, however, was essentially constant at –7.3 mV h^–1±3.7 mV h^–1 per 10¹⁰ viable cells during growth under conditions of constant dissolved oxygen tension and constant pH. Using these observations, the quantity of reductants synthesized and secreted into the medium by viable hybridoma cells was estimated to be approximately 1.3 mole h^–1 per 10¹⁰ viable hybridoma cells. The time course of specific monoclonal antibody secretion rate did not correlate with changes in the external oxidation/reduction potential in either serum containing or protein-free medium.     

Determination of cell lysis and death kinetics in continuous hybridoma cultures from the measurement of lactate dehydrogenase release

The death of the hybridoma VO 208 in a continuous culture at pH 7 and 6.8 was investigated by measuring both the appearance of visible dead cells which do not exclude the trypan blue dye and the release of lactate dehydrogenase (LDH) in the culture medium. The intracellular LDH was found to be completely released either when live cells lysed or when they were transformed into visible dead cells. No significant lysis of blue dead cells could be observed at the two different pH. Using a LDH balance over the culture system, cell lysis was found negligible at pH 7, but accounted for 20% of the total cell death at pH 6.8. A methodology is proposed to evaluate the rate constants of hybridoma lysis and total death. For the investigated cell line in continuous culture, the calculated total cell death rate constant was found to increase from 0.002 h^–1 to 0.01 h^–1 when decreasing the pH from 7 to 6.8.Abbreviations D dilution rate (h^–1) - k_b specific trypan-blue dead cells appearance rate (h^–1) - k_L specific lysis rate of viable cells (h^–1) - k_d specific death rate (h-1) - LDH₀ lactate dehydrogenase activity in the feed culture medium (IU.l^–1) - LDH lactate dehydrogenase activity in the outlet culture medium (IU.l^–1) - LDH_i intracellular lactate dehydrogenase activity of viable cells (IU.10^–9 cells) - r_LDH total rate of LDH release (IU.h^–1.L^–1) - r_b transformation rate of viable cells into blue dead cells (10⁹ cells.h^–1.L^–1) - x_v viable cell concentration (10⁹ cells.l^–1) - x_b trypan-blue dead cell concentration (10⁹ cells.l^–1)     

Cyclic AMP-dependent regulation of activities of synthetase and phosphodiesterase of 2′,5′-oligoadenylate in NIH 3T3 cells

Summary Dihydrofolate synthetase (EC 6.3.2.12) from N. gonorrhoeae was isolated and enzyme characteristics were determined. The purified enzyme was found quite stable when stored at –60 °C. About 50% of the enzyme activity wag destroyed within 6 weeks when kept at 4 °C. Maximum velocity was observed at pH 9.3. The enzyme required a monovalent cation, K⁺ or NH₄ ⁺ , and divalent cation, Mg²⁺ or Mn²⁺ for its function. ATP at 5 mM concentration gave maximum activity. K_m values for dihydropteroate and L-glutamate at pH 9.3 were 3.5 × 10^–5 M and 6.5 × 10^–4 M, respectively. Patterns of product inhibition by dihydrofolate were found to be non-competitive with respect to dihydropteroate, having a K_i value of 5.1 ± 0.8 × 10^–4 M, and competitive with respect to L-glutamate, having a K_i value of 6.2 × 10^–4 M.     

Modeling of the pyruvate production with<Emphasis Type="Italic"> Escherichia coli</Emphasis> in a fed-batch bioreactor

A family of 10 competing, unstructured models has been developed to model cell growth, substrate consumption, and product formation of the pyruvate producing strain Escherichia coli YYC202 ldhA::Kan strain used in fed-batch processes. The strain is completely blocked in its ability to convert pyruvate into acetyl-CoA or acetate (using glucose as the carbon source) resulting in an acetate auxotrophy during growth in glucose minimal medium. Parameter estimation was carried out using data from fed-batch fermentation performed at constant glucose feed rates of q_VG=10 mL h^–1. Acetate was fed according to the previously developed feeding strategy. While the model identification was realized by least-square fit, the model discrimination was based on the model selection criterion (MSC). The validation of model parameters was performed applying data from two different fed-batch experiments with glucose feed rate q_VG=20 and 30 mL h^–1, respectively. Consequently, the most suitable model was identified that reflected the pyruvate and biomass curves adequately by considering a pyruvate inhibited growth (Jerusalimsky approach) and pyruvate inhibited product formation (described by modified Luedeking–Piret/Levenspiel term).List of symbols c_A acetate concentration (g L^–1) - c_A,0 acetate concentration in the feed (g L^–1) - c_G glucose concentration (g L^–1) - c_G,0 glucose concentration in the feed (g L^–1) - c_P pyruvate concentration (g L^–1) - c_P,max critical pyruvate concentration above which reaction cannot proceed (g L^–1) - c_X biomass concentration (g L^–1) - K_I inhibition constant for pyruvate production (g L^–1) - K_I^A inhibition constant for biomass growth on acetate (g L^–1) - K_P saturation constant for pyruvate production (g L^–1) - K_P inhibition constant of Jerusalimsky (g L^–1) - K_S^A Monod growth constant for acetate (g L^–1) - K_S^G Monod growth constant for glucose (g L^–1) - m_A maintenance coefficient for growth on acetate (g g^–1 h^–1) - m_G maintenance coefficient for growth on glucose (g g^–1 h^–1) - n constant of extended Monod kinetics (Levenspiel) (–) - q_V volumetric flow rate (L h^–1) - q_VA volumetric flow rate of acetate (L h^–1) - q_VG volumetric flow rate of glucose (L h^–1) - r_A specific rate of acetate consumption (g g^–1 h^–1) - r_G specific rate of glucose consumption (g g^–1 h^–1) - r_P specific rate of pyruvate production (g g^–1 h^–1) - r_P,max maximum specific rate of pyruvate production (g g^–1 h^–1) - t time (h) - V reaction (broth) volume (L) - Y_P/G yield coefficient pyruvate from glucose (g g^–1) - Y_X/A yield coefficient biomass from acetate (g g^–1) - Y_X/A,max maximum yield coefficient biomass from acetate (g g^–1) - Y_X/G yield coefficient biomass from glucose (g g^–1) - Y_X/G,max maximum yield coefficient biomass from glucose (g g^–1) - growth associated product formation coefficient (g g^–1) - non-growth associated product formation coefficient (g g^–1 h^–1) - specific growth rate (h^–1) - _max maximum specific growth rate (h^–1)     

Effect of nutrient deficiency on accumulation and relative molecular weight of poly-β-hydroxybutyric acid by methylotrophic bacterium,Pseudomonas 135

Summary Pseudomonas 135, a facultative methylotroph, was cultivated on methanol as a sole carbon and energy source for the accumulation of poly--hydroxybutyric acid (PHB). The cells grew fairly well on minimal synthetic medium containing 0.5% (v/v) of methanol at pH 7.0 and 30° C. The maximum specific growth rate was determined to be 0.26–0.28 h^–1 with a growth yield of 0.38 in the optimized growth medium. For stimulation of PHB accumulation in the cells, deficiency of nutrients such as NH _inf4 ^sup+ , Mg²⁺ and PO _inf4 ^sup3– was crucial even though cell growth was significantly suppressed. The PHB content of a 40-h culture was determined to be 37% of the total cell mass in NH _inf4 ^sup+ -limited medium, 42.5% on Mg²⁺-deficient medium, and 34.5% on PO _inf4 ^sup3– -deficient medium. The maximum content of PHB in the cells could reach 55% in NH _inf4 ^sup+ -limited fed-batch culture. The average relative molecular eight determined by gel permeation chromatography was 3.7 × 10⁵ in NH _inf4 ^sup+ -limited culture, 2.5 × 10⁵ in Mg²⁺-deficientmedium, and 3.1 × 10⁵ in PO _inf4 ^sup3– -deficient medium. Polydispersity determined in each culture was relatively high (about 10–11). The solid PHB had a melting temperature of 173° C. Correspondence to: J. M. Lebeault     

The influence of flow rate and the composition of supplied CO2/air mixtures on discontinuous growth of Tetraselmis sp.

Summary This paper studies the influence of the flow rate of gaseous mixtures on the kinetics of growth and the fatty acid composition of Tetraselmis sp. at CO₂/air ratios of 3 × 10^–4 and 2 × 10^–5. The specific growth rate rises with increased flow rate up to values of approximately 0.086 h^–1 and 0.063 h^–1 at CO₂/air ratios of 3 × 10^–4 and 2 × 10^–5 respectively, when the flow rate is approximately 3 v/v per minute. At higher flow rates, the specific growth rate decreases. The polyunsaturated fatty acid content decreases slightly as the gaseous mixture flow rate increases, whereby the ratio 3/6 remains between 2 and 3, indicating good nutritional values. Offprint requests to: E. Molina     

Frog striated muscle is permeable to hydroxide and buffer anions

Hydroxide, bicarbonate and buffer anion permeabilities in semitendinosus muscle fibers of Rana pipiens were measured. In all experiments, the fibers were initially equilibrated in isotonic, high K₂SO₄ solutions at pH _o =7.2 buffered with phosphate. Two different methods were used to estimate permeabilities: (i) membrane potential changes were recorded in response to changes in external ion concentrations, and (ii) intracellular pH changes were recorded in response to changes in external concentrations of ions that alter intracellular pH. Constant field equations were used to calculate relative or absolute permeabilities.In the first method, to increase the size of the membrane potential change produced by a sudden change in anion entry, external K⁺ was replaced by Cs⁺ prior to changes of the anion under study. At constant external Cs⁺ activity, a hyperpolarization results from increasing external pH from 7.2 to 10.0 or higher, using either CAPS (3-[cyclohexylamino]-1-propanesulfonic acid) or CHES (2-[N-cyclohexylamino]-ethanesulfonic acid) as buffer. For each buffer, the protonated form is a zwitterion of zero net charge and the nonprotonated form is an anion. Using reported values of H⁺ permeability, calculations show that the reduction in [H⁺] _o cannot account for the hyperpolarizations produced by alkaline solutions. Membrane hyperpolarization increases with increasing total external buffer concentration at constant external pH, and with increasing external pH at constant external buffer anion concentration. Taken together, these observations indicate that both OH^– and buffer anions permeate the surface membrane. The following relative permeabilities were obtained at pH_o, 10.0± 0.3: (P_OH/P_K) = 890 ± 150, (P_CAPS/P_K) = 12 ± 2 (P_CHIES/P_K) = 5.3 ± 0.9, and (P_NO3/P_K) = 4.7 ± 0.5 P_NO/P_K was independent of pH _o up to 10.75. At pH_o = 9.6, (P_HCO3/P_K) = 0.49 ± 0.03; at pH _o = 8.9, (P_Cl/P_K) = 18± 2 and at pH _o = 7.1, (P_HEPES/P_K) = 20 ± 2.In the second method, on increasing external pH from 7.2 to 10.0, using 2.5 mm CAPS (total buffer concentration), the internal pH increases linearly with time over the next 10 min. This alkalinization is due to the entry of OH^– and the absorption of internal H⁺ by entering CAPS^– anion. The rate of CAPS^– entry was determined in experiments in which the external CAPS concentration was increased at constant external pH. Such increases invariably produced an increase in the rate of internal alkalinization, which was reversed when the CAPS concentration was reduced to its initial value. From the internal buffer power, the diameter of the fiber under study and the rates of change of internal pH, the absolute permeability for both OH^– and CAPS^– were calculated. At external pH = 10.0, the average (±sem) permeabilities were: P_OH=1.68±0.19×10^–4 cm/sec and P_CAPS=2.10±0.74×10^–6cm/sec.We conclude that OH^– is about 50 times more permeable than Cl^– at alkaline pH and that the anionic forms of commonly used buffers have significant permeabilities.This research was supported by a grant from the National Institutes of Health (AR 31814). The authors wish to thank Dr. Peter G. Shrager and Dr. Bruce C. Spalding for reading an early draft of this report and for providing helpful suggestions.     

Influence of temperature rise on kinetic parameters during batch propagation of Kluyveromyces fragilis in cheese whey under ambient conditions

Three 5 l working volume fermenters were used to investigate the growth of the yeast Kluyveromyces fragilis in acid cheese whey under ambient temperature in order to assess the specific growth rate and yield, the lactose and oxygen uptake rates during the various phases of batch culture, the effect of increasing temperature on the various kinetic parameters, and the need for a cooling unit for single cell production batch systems. The initial dissolved oxygen in the medium was 5.5 mg l^–1 and the pH was maintained at 4.5. The observed lag phase, specific growth rate and maximum cell number were 4 h, 0.2 h^–1 and 8.4 × 10⁸ cells ml^–1, respectively. About 99% of the lactose in cheese whey was utilized within 20 h, 85% during the exponential growth phase. The specific lactose utilization rates by K. fragilis were 0.20 × 10^–12, 1.457 × 10^–12, 0.286 × 10^–12 and 0.00 g lactose cell^–1 h^–1, for the lag, exponential, stationary and death phases, respectively. The dissolved oxygen concentration in the medium decreased as the cell number increased. The lowest oxygen concentration of 1.2 mg l^–1 was observed during the stationary phase. The volumetric oxygen transfer coefficient was 0.41 h^–1 and the specific oxygen uptake rates were 0.32 × 10^–12, 2.14 × 10^–12, 0.51 × 10^–12 and 0.003 × 10^–12 mg O₂ cell^–1 h^–1, for the lag, exponential, stationary and death phases, respectively. The maximum temperature recorded for the medium was 33 °C, indicating that a cooling unit for batch production of single cell protein at ambient temperature is not needed for this type of bioreactor. The increase in medium temperature affected the cell growth and the lactose and oxygen uptake rates.     

Ethylene metabolism in Pisum sativum L.: Kinetic parameters,the effects of propylene,silver and carbon dioxide and comparison with other systems

The kinetic parameters of in vivo ethylene metabolism by seedlings of Pisum sativum L. cv. Alaska have been determined. The oxidation of ethylene to CO₂, (Ox) and the incorporation of ethylene into the tissue (TI) were both shown to display Michaelis-Menten kinetics (K_m Ox = 0.9 × 10^–6 M liquid phase, V_max Ox = 2.4 × 10^–10 moles g^– dry mass h^–1 K_m TI = 1.6 × 10^–6 M liquid phase, V_max TI = 4.5 × 10^–10 moles g^–1 dry mass h^–1). Propylene competitively inhibited both Ox (K_i = 7.0 × 10^–6 M) and TI (K_i = 3.7 × 10^–7 M). A system comparable to Ox was absent from imbibed cotyledons of Vicia faba L. cv. Aquadulce even at saturating concentrations of ethylene similar to those used in kinetic analysis on Pisum. Silver ions were shown to inhibit TI but promoted Ox, while carbon dioxide inhibited Ox but promoted TI. Kinetic data on both these effects are presented. Data on the effect of a range of concentrations of CO₂ on TI and Ox are also presented.To whom editorial correspondence should be sent     

Nitrate reductase from yeast: cultivation,partial purification and characterization

Summary Several yeast strains were assayed for occurence of nitrate reductase after growth in a defined medium with nitrate as the sole nitrogen source, Candida boidinii DSM 70026, showing the highest specific activity, was further investigated. The procedures for yeast fermentation and nitrate reductase purfication are described in detail. Nitrate reductase from this yeast was characterized as NAD(P)H: nitrate oxidoreductase (E.C.1.6.6.2). The enzyme activity with NADH (NADPH) was highest at pH 7.0 (7.1) and 30° C (25° C). The values of K _m determinations with NADH/NADPH were both 4 × 10^–4 mol/l; values for the substrate inhibition constant (K _i) were 6 × 10^–4 mol/l. The molecular mass of the native enzyme was estimated by gel permeation chromatography to be approximately 350 kDa. Offprint requests to: R. Gromes     

Studies on the variables and kinetics of SCP production from nopal fruit juice

Summary Submerged batch cultivation under controlled environmental conditions of pH 3.8, temperature 30°C, and K_La200 h^–1 (above 180 mMO₂ l ^–1 h^–1 oxygen supply rate) produced a maximum (12.0 g·l ^–1) SCP (Candida utilis) yield on the deseeded nopal fruit juice medium containing C/N ratio of 7.0 (initial sugar concentration 25 g·l ^–1) with a yield coefficient of 0.52 g cells/g sugar. In continuous cultivation, 19.9 g·l ^–1 cell mass could be obtained at a dilution rate (D) of 0.36 h^–1 under identical environmental conditions, showing a productivity of 7.2 g·l ^–1·h^–1. This corresponded to a gain of 9.0 in productivity in continuous culture over batch culture. Starting with steady state values of state variables, cell mass (C_X–19.9 g·l ^–1), limiting nutrient concentration (C_ln–2.5 g·l ^–1) and sugar concentration (C_S–1.5 g·l ^–1) at control variable conditions of pH 3.8, 30°C, and K_La 200 h^–1 keeping D=0.36 h^–1 as reference, transient response studies by step changes of these control variables also showed that this pH, temperature and K_La conditions are most suitable for SCP cultivation on nopal fruit juice. Kinetic equations obtained from experimental data were analysed and kinetic parameters determined graphically. Results of SCP production from nopal fruit juice are described.Nomenclature C_ln concentration of ammonium sulfate (g·l ^–1) - C_S concentration of total sugar (g·l ^–1) - C_X cell concentration (g·l ^–1) - D dilution rate (h^–1) - K_ln Monod's constant (g·l ^–1) - m maintenance coefficient (g ammonium sulfate cell^–1 h^–1) - m_(S) maintenance coefficient (g sugar g cell^–1 h^–1) - t time, h - Y yield coefficient (g cells/g ammonium sulfate) - Y_m maximum of Y - Y_S yield coefficient based on sugar consumed (g cells · g sugar^–1) - Y_S(m) maximum value of Y_S - ^µm maximum specific growth rate constant (h^–1)     

Effect of light intensity and ammonium-N on carotenogenesis ofTrentepohlia odorata andDunaliella bardawil

AxenicTrentepohlia odorata was cultured at three different NH₄Cl levels (3.5 × 10^–2, 3.5 × 10^–3, 3.5 × 10^–4 M) and three different light intensities (48, 76, 122 µmol m^–2 s^–1). Chloride had no effect on growth over this range of concentration. High light intensity and high NH₄Cl concentration enhanced the specific growth rate. The carotenoid content increased under a combination of high light intensity and low N concentration. WhenD. bardawil was exposed to the same combination of growth conditions, there was an increase in its carotenoid content. The light saturation and the light inhibition constants (K _s andK _i, respectively) for growth, and the saturation constant (K _m) for NH₄Cl were determined. TheK _s andK _i values were higher inT. odorata (66.7 and> 122 mol m^–2 s^–1, respectively) than inD. bardawil (5.1 and 14.7 µmol m^–2 s^–1, respectively). TheK _m value determined at 122 µmol m^–2 s^–1, however, was lower inT. odorata (0.048 µM) than inD. bardawil (0.062 µM).Author for correspondence     

Low responder MHC alleles for Tc recognition of influenza nucleoprotein

Since virus nucleoprotein is an important target antigen for antiinfluenza cytotoxic T cells (Tc), we examined the genetics of Tc responses to this single viral protein to find three nonresponder alleles (D ^d, D ^k, and K ^b) in three haplotypes and their recombinants so far tested. B10.A(5R) mice bearing nonresponder MHC class I antigen in the D and K regions show no anti-NP Tc responses, however they do show a strong A-virus cross-reactive anti-influenza cytotoxicity. The high frequency of nonresponsiveness to a single viral component, as compared with the entire virus, has implications for the development of simple vaccines.Abbreviations used in this paper DMEM/5 Dulbecco's modified Eagle's medium + 5% FCS + penicillin, streptomycin, L-glutamine - FCS fetal calf serum - HA influenza hemagglutinin - HAU hemagglutinating units - H1.VAC vaccinia recombinant containing a copy of the 1934 H1 gene - i. n. intranasally - MHC major histocompatibility complex - m. o. i. multiplicity of infection - NA influenza neuraminidase - NP influenza nucleoprotein - NP.VAC vaccinia recombinant containing a copy of the 1934 NP gene - p. f. u. plaque-forming units - RPMI/10 RPMI 1640 + 10% FCS + penicillin, streptomycin, L-glutamine, 5 × 10^–5 M 2-mercaptoethanol - Tc cytotoxic T cells     

Protein production from whey usingPenicillium cyclopium; growth parameters and cellular composition

Summary The growth parameters ofPenicillium cyclopium have been evaluated in a continuous culture system for the production of fungal protein from whey. Dilution rates varied from 0.05 to 0.20 h^–1 under constant conditions of temperature (28°C) and pH (3.5). The saturation coefficients in the Monod equation were 0.74 g l^–1 for lactose and 0.14 mg l^–1 for oxygen, respectively. For a wide range of dilution rates, the yield was 0.68 g g^–1 biomass per lactose and the maintenance coefficient 0.005 g g^–1 h^–1 lactose per biomass, respectively. The maximum biomass productivity achieved was 2 g l^–1 h^–1 biomass at dilution rates of 0.16–0.17 h^–1 with a lactose concentration of 20 g l^–1 in the feed. The crude protein and total nucleic acid contents increased with a dilution rate, crude protein content varied from 43% to 54% and total nucleic acids from 6 to 9% in the range of dilution rates from 0.05 to 0.2 h^–1, while the Lowry protein content was almost constant at approximately 37.5% of dry matter.Nomenclature (mg l^–1) C_o initial concentration of dissolved oxygen - (h^–1) D dilution rate - (mg l^–1) K₀₂ saturation coefficient for oxygen - (g l^–1) K_s saturation coefficient for substrate - (g g^–1 h^–1) lactose per biomass) m maintenance energy coefficient - (mM g^–1 h^–1O₂ per biomass) Q₀₂ specific oxygen uptake rate - (g l^–1) S residual substrate concentration at steady state - (g l^–1) S_o initial substrate concentration in feed - (min) t_1/2 time when C_o is equal to C_o/2 - (g l^–1) X biomass concentration - (g l^–1) X biomass concentration at steady state - (g g^–1 biomass per lactose) Y_G yield coefficient for cell growth - (g g^–1 biomass per lactose) Y_x/s overall yield coefficient - (h^–1) specific growth rate     

Medium optimization for a methanol utilizing bacterium based on chemostat theory

Summary In the productions of biomass and vitamin B₁₂ using methanol as the sole carbon source, it is necessary to use a medium in which methanol is the growth limiting substrate. Other inorganic salts should be in slight excess so that the yield of cells and the intracellular content of vitamin B₁₂ do not vary. From basic principles of chemostat culture, a medium was optimized for Pseudomonas AM-1 a methanol utilizing bacterium, for the concentrations of various inorganic salts. This was done in a series of chemostat cultures at a dilution rate of 0.1 h^–1. Optimum amounts of NH₄ ⁺, PO₄ ^3- and Mg²⁺ were estimated from the minimum concentration of the salt at which methanol became growth limiting. The optimum concentrations of Ca²⁺, Fe²⁺, Mn²⁺, and Zn²⁺ as a group were determined in the same way. Cu²⁺, Mo⁶⁺, Co²⁺ and B³⁺ are required at concentrations of g/l and they were not studied as these very low level can be introduced as contaminants from other salts. The optimum medium composition (in g/l) was as follows: (NH₄)₂SO₄, 1.0; H₃PO₄, 75×10^–3; MgSO₄ · 7H₂O, 30×10^–3; CaCl₂ · 2H₂O, 3.3×10^–3; FeSO₄ · 7H₂O, 1.3×10^–3, MnSO₄ · 4H₂O, 0.13×10^–3; ZnSO₄ · 7H₂O, 0.13×10^–3; CuSO₄ · 5H₂O, 40×10^–6; Na₂MoO₄, 40×10^–6; CoCl₂ · 6H₂O, 40×10^–6; H₃BO₃, 30×10^–6 and methanol 4.     

Interactions of growth inhibitory factor with hydroxyl and superoxide radicals

To show the effects of growth inhibitory factor (Cu₄Zn₃MT-III) involved in the scavenging of reactive oxygen species (ROS), a pulse radiolytic study was employed using N₂O-saturated Cu₄Zn₃MT-III aqueous solutions. It was demonstrated that the oxidizing OH radical efficiently reacted with Cu₄Zn₃MT-III by forming a thiyl radical RS with a second-order constant of 1.46×10¹¹ mol l^–1s^–1, which was determined by competition kinetics against KSCN. The thiyl radical RS reacted rapidly and reversibly with a thiolate in Cu₄Zn₃MT-III to form radical anion RSSR ^– with a constant of 1.65×10⁹ mol lL^–1s^–1 per thiolate, while the constant of the decay of this radical anion was 2.72×10⁵ s^–1, and the equilibrium constant of the formation for RSSR ^– was 6.08×10³ mol^–1 l. These values were close to those of Cd₅Zn₂MT-II. The SOD activity of Cu₄Zn₃MT-III to quench O₂ ^–was assayed by the riboflavine-methionine-nitrobluetetrazolium (NBT) method which catalyzed the dismutation of superoxide (O₂ ^–) at pH 7.8 with an IC₅₀ value of 1.50×10^–6 M for Cu₄Zn₃MT-III and 1.62×10^–6 M for Cd₅Zn₂MT-II. Additionally, the down-regulation of GIF may be a main factor in the decrease of the scavenging ability for the free OH and O₂ ^–radicals, which is possibly associated with the pathogenesis of neurodegenerative disease.     

Feasibility study on the use of hyperosmolar medium for improved antibody production of hybridoma cells in a long-term,repeated-fed batch culture

To test the feasibility of using hyperosmolar medium for improved antibody production in a long-term, repeated fed-batch culture, the influence of various culture conditions (serum concentration and cultivation method) on the hybridoma cells' response to hyperosmotic stress resulting from sodium chloride addition was first investigated in a batch culture. The degree of cell growth depression resulting from hyperosmotic stress was dependent on serum concentrations and cultivation methods (static and agitated cultures). Depression of cell growth was most significant in agitated cultures with low serum concentration. However, regardless of serum concentrations and cultivation methods used, the hyperosmotic stress significantly increased specific antibody productivity (q _MAb). Increasing osmolality from 284 to 396 mOsm kg^–1 enhanced the q_MAb in agitated cultures with 1% serum by approximately 124% while the similar osmotic stress enhanced the q _MAb in static cultures with 10% serum by approximately 153%. Next, to determine whether this enhanced q_MAb resulting from hyperosmotic stress can be maintained after adaptation, long-term, repeated-fed batch cultures with hyperosmolar media were carried out. The cells appeared to adapt to hyperosmotic stress. When a hyperosmolar medium (10% serum, 403 mOsmkg^–1) was used, the specific growth rate improved gradually for the first four batches and thereafter, remained constant at 0.040±0.003 (average ± standard deviation) hr^–1 which is close to the value obtained from a standard medium (10% serum, 284 mOsmkg^–1) in the batch culture. While the cells were adpating to hyperosmotic stress, the q_MAb was gradually decreased from 0.388×10^–6 to 0.265×10^–6 g cell hr^–1 and thereafter, remained almost constant at 0.272±0.014× 10^–6 g cell^–1 hr^–1. However, this reduced q _MAb after adaptation is still approximately 98% higher than the q_MAb obtained from a standard medium in the batch culture.The authors would like to thank Dr.M. Kaminski for providing the hybridoma cell line used in this study. This work was supported by the Korea Science and Engineering Foundation.     

Mixed inhibitions by methanol, furfural and acetic acid on xylitol production by Candida guilliermondii

Xylose production by Candida guilliermondii FTI 20037 was carried out in a synthetic medium in the presence of 0–100 g methanol l^–1, 0–0.7 g furfural l^–1 or 0–1.3 g acetic acid l^–1. Kinetic results show a mixed inhibition mechanism in all three cases. Maximum specific productivity and saturation constant for product formation were, in the absence of inhibition, 3.6 g_P g_X ^–1 h^–1 and 232 g_S l^–1, respectively, while the inhibition constants, K _i and K _i, were 17 and 50 g methanol l^–1, 0.62 and 7.0 g furfural l^–1, 0.69 and 3.5 g acetic acid l^–1, which suggests the following order of inhibition: furfural > acetic acid > methanol.     

Influence of exponentially decreasing feeding rates on fed-batch ethanol fermentation of sugar cane blackstrap molasses

Summary The ethanol yield was not affected and the ethanol productivity was increased when exponentially decreasing feeding rates were used instead of constant feeding rates in fed batch ethanol fermentations. The influences of the initial sugar feeding rate on the ethanol productivity, on the constant ethanol production rate during the feeding phase and on the initial ethanol production specific rate are represented by Monod-like equations.Nomenclature F reactor feeding rate (L.h^–1) - F_o initial reactor feeding rate (L.h^–1) - K time constant; see equation (l) (h^–1) - M_E mass of ethanol in the fermentor (g) - M_s mass of TRS in the fermentor (g) - M_x mass of yeast cells (dry matter) in the fermentor (g) - P ethanol productivity (g.L^–1.h^–1) - R ethanol constant production rate during the feeding phase (g.h^–1) - s standard deviation - S_o TRS concentration in the feeding mash (g.L^–1) - t time (h) - T fermentor filling-up-time (h) - T time necessary to complete the fermentation (h) - TRS total reducing sugars calculated as glucose (g.L^–1) - V_o volume of the inoculum (L) - V_f final volume of medium in the fermentor (L) - X_o yeast concentration of the inoculum (dry matter) (g.L^–1) - ethanol yield (% of the theoretical value) - initial specific rate of ethanol production (h^–1)     

In vitro Proliferation of Human Bone Marrow Mesenchymal Stem Cells Employing Donor Serum and Basic Fibroblast Growth Factor

A method for the in vitro proliferation of human bone marrow mesenchymal stem cells (MSCs) employing a medium not containing fetal calf serum (FCS) was developed for a regenerative medicine of cartilage using MSCs. Without using density-gradient centrifugation, the bone marrow aspirate was poured into a dish (6.0 \times 10⁵ nucleated cells/cm²) with DMEM medium containing 10% serum (FCS or donor serum) and basic fibroblast growth factor, and incubated at 37 °C under a 5% CO₂ atmosphere. The density of adhesive cells incubated with the medium containing human serum and basic fibroblast growth factor (10 ng/ml) almost reached confluence at 19d and was 1.4-2.7 times that in the medium containing only FCS. The density of cells incubated with the medium containing only human serum was 0.1-0.6 times that in the medium containing only FCS. The content of CD45^- CD105⁺ cells among the cells harvested after a 19-d incubation in the medium containing human serum and basic fibroblast growth factor was higher than 90%. This high content and chondrogenic activity, which was confirmed by pellet cultivation and staining with Safranine O, were maintained even after further subcultivation in the medium to 17 population doubling levels. Consequently, this method might be applicable to in vitro proliferation of MSCs for the regeneration of cartilage.